Method of producing catalytic material for fabricating nanostructures

ABSTRACT

Methods of fabricating nano-catalysts are described. In some embodiments the nano-catalyst is formed from a powder-based substrate material and is some embodiments the nano-catalyst is formed from a solid-based substrate material. In some embodiments the substrate material may include metal, ceramic, or silicon or another metalloid. The nano-catalysts typically have metal nanoparticles disposed adjacent the surface of the substrate material. The methods typically include functionalizing the surface of the substrate material with a chelating agent, such as a chemical having dissociated carboxyl functional groups (—COO), that provides an enhanced affinity for metal ions. The functionalized substrate surface may then be exposed to a chemical solution that contains metal ions. The metal ions are then bound to the substrate material and may then be reduced, such as by a stream of gas that includes hydrogen, to form metal nanoparticles adjacent the surface of the substrate.

CROSS REFERENCE TO RELATED APPLICATION

This application is a divisional of U.S. Pat. No. 8,377,840, filed Feb.13, 2009, and entitled “Method of Producing Catalytic Materials forFabricating Nanostructures,” the entire contents of which areincorporated by reference herein.

GOVERNMENT RIGHTS

The U.S. Government has rights to this invention pursuant to contractnumber DE-AC05-00OR22800 between the U.S. Department of Energy andBabcock & Wilcox Technical Services Y-12, LLC.

This invention was made with government support under Contract No.DE-AC05-00OR22725 awarded by the U.S. Department of Energy. Thegovernment has certain rights in the invention.

FIELD

This disclosure relates to the field of catalytic materials. Moreparticularly, this disclosure relates to catalytic materials for thefabrication of nanostructures.

BACKGROUND

Nanostructures are objects that have physical dimensions between thoseof sub-atomic-scale (less than one Angstrom-sized) structures andmicroscopic-scale (greater than one tenth micrometer-sized) structures.Nanostructures are said to have nano-scale features. “Nano-scale” refersto a dimension that is between approximately one Angstrom (0.1nanometer) and approximately 100 nanometers (0.1 micrometer). Nano-scalefeatures may occur in one, two, or three dimensions. For example,nano-textured surfaces have one nano-scale dimension. That is, suchsurfaces have nano-features such as ridges, valleys or plateaus thatprovide surface height variations that range from about 0.1 to about 100nanometers. Another example of a one-dimension nanostructure is a filmthat has a thickness that ranges from about 0.1 to about 100 nanometers.Nanotubes are examples of nanostructures that have two nano-scaledimensions. That is, a nanotube has a diametral dimension and a length.The diametral dimension of a nanotube ranges from about 0.1 to about 100nanometers. The length of a nanotube may be greater than hundreds ofmicrons. Nanoparticles have three diametral nano-scale dimensions. Eachdiametral dimension of a nanoparticle ranges from about 0.1 to about 100nm.

Nanostructures may be formed from carbon, silicon, boron, various metaland metalloid elements, various compounds, alloys and oxides of thoseelements, ceramics, various organic materials including monomers andpolymers, and potentially any other material. Nanostructures havepotential use in various physical, chemical, mechanical, electronic andbiological applications. Nanomaterials are collections ofnanostructures. The formation, collection, and assembly of nanomaterialsgenerally involve difficult and expensive processes. One major issuewith nanomaterials is the difficulty of production of the nanostructuresin sufficient quantity, purity, and uniformity of morphology to beuseful. What are needed therefore are better systems and methods formanufacturing nanomaterials.

SUMMARY

In one embodiment the present disclosure provides a method offabricating a nano-catalyst that includes a step of contacting a metalpowder with a first solution comprising a complexing agent to produce acomplexed metal powder and a residual first solution. A further stepincludes separating the complexed metal powder and a substantial portionof the residual first solution from each other. The method proceeds witha step of contacting the complexed metal powder with a second solutioncomprising metal ions to produce (i) a loaded metal powder wherein atleast a portion of the metal ions are bound to the complexed metalpowder and (ii) a residual second solution. The method typicallyincludes separating the loaded metal powder and substantially all of theresidual second solution from each other to produce a dry loaded metalpowder, and then contacting the metal ions bound to the complexed metalpowder with a reducing atmosphere to form the nano-catalyst as metalnanoparticles on the metal powder.

In some embodiments employing a metal powder, the complexing agentincludes a chelating agent and in some embodiments the complexing agentincludes a coupling agent. In various embodiments the metal powder mayinclude NiAl. In some embodiments where the metal powder includes NiAlthe metal ions may include Fe³⁺. In some embodiments, regardless of thesubstrate, the metal ions may include Fe³⁺, Ni²⁺, Co²⁺, or Co³⁺.

Further provided herein is a method of fabricating a nano-catalyst thatbegins with providing a microemulsion medium comprising a surfactant,water, and an organic compound selected from the group consisting ofhexanol, cyclohexane, and a combination thereof. The method includes afurther step of contacting an organic silane with the microemulsion toform silicon dioxide nanoparticles, and a step of contacting the silicondioxide particles with a complexing agent to form complexed silicondioxide nanoparticles. The method typically proceeds with contacting thecomplexed silicon dioxide nanoparticles with a solution comprising metalions to produce (i) loaded silicon dioxide nanoparticles wherein atleast a portion of the metal ions are bound to the complexed silicondioxide nanoparticles and (ii) a residual solution. The method thenprovides the steps of separating the loaded silicon dioxidenanoparticles and substantially all of the residual solution from eachother to produce dry loaded silicon dioxide nanoparticle, and contactingthe metal ions bound to the complexed silicon dioxide nanoparticles witha reducing atmosphere to form the nano-catalyst as metal nanoparticleson the silicon dioxide nanoparticles.

In some embodiments employing the aforementioned microemulsion mediumthe complexing agent includes a chelating agent and in some embodimentsthe complexing agent includes a coupling agent. In various embodimentsthe metal powder may include NiAl. In some embodiments where the metalpowder includes NiAl the metal ions may include Fe³⁺. In someembodiments, regardless of the substrate, the metal ions may includeFe³⁺, Ni²⁺, Co²⁺, or Co³⁺.

Further provided is a method of fabricating a nano-catalyst thattypically begins with a step of washing substrate material that includessilicon with one or more materials selected from the group consisting ofethanol, acetone, chloroform, and water to form a treated substratematerial. Further steps provide for contacting the treated substratematerial with nitric acid to provide an activated substrate material andthen contacting the treated substrate material with a complexing agentto provide a complexed substrate material. A further step includescontacting the complexed substrate material with metal ions wherein atleast a portion of the metal ions are bound to the complexed substratematerial and then a final step provides for contacting the metal ionsbound to the complexed substrate material with a reducing atmosphere toform the nano-catalyst as metal nanoparticles on the substrate material.

In some embodiments employing silicon substrate material the substratematerial includes a silicon wafer.

In some embodiments employing silicon substrate material the complexingagent includes a chelating agent and in some such embodiments thecomplexing agent includes a coupling agent. Sometimes the complexingagent comprises a mixture of chloroform and a silane compound.

Further provided is a method of fabricating a metal-powder-basednano-catalyst that includes contacting a metal powder with a solutionthat includes metal ions from a metal salt having an anion and thatincludes an acid comprising the anion of the metal salt to form loadedmetal powder comprising metal ions, separating the loaded metal powderand substantially all of the solution that includes metal ions from eachother; and reducing the metal ions to form the metal-powder-basednano-catalyst. In some of these embodiments the solution that includesthe metal ions includes a metal salt selected from the group consistingof an iron salt, a nickel salt, a cobalt salt, and combinations of twoor more of the foregoing. Sometimes the solution that includes the metalions includes two or more metal salts selected from the group consistingof an iron salt, a nickel salt, and a cobalt salt and combinations oftwo or more of the foregoing. Some embodiments of this method furtherinclude a step of activating the surface of a metal powder and thenthese embodiments proceed with contacting the metal powder with asolution comprising metal ions to form loaded metal powder comprisingmetal ions.

Further provided is a method of fabricating a nano-catalyst that beginswith etching a substrate comprising a metal selected from the groupconsisting of scandium, titanium, vanadium, chromium, manganese, iron,cobalt, nickel, copper, and zinc with an etchant selected from the groupconsisting of an aqueous solution of an aluminum salt, a dilute acid,and a combination thereof, wherein metal ions from the substrate form inthe etchant. This method proceeds with drying the substrate in thepresence of the etchant, wherein nano-size deposits comprising the metalions are deposited adjacent the surface of the substrate. The methodconcludes with reducing the metal ions to produce the nano-catalyst. Insome of these embodiments the substrate includes nickel and the etchantis selected from the group consisting of an aqueous solution of achloride salt of aluminum, dilute hydrochloric acid, and combinationsthereof. In some of these embodiments the substrate comprises nickel andthe etchant is selected from the group consisting of an aqueous solutionof a nitrate salt of aluminum salt, dilute nitric acid, and combinationsthereof.

BRIEF DESCRIPTION OF THE DRAWINGS

Various advantages are apparent by reference to the detailed descriptionin conjunction with the figures, wherein elements are not to scale so asto more clearly show the details, wherein like reference numbersindicate like elements throughout the several views, and wherein:

FIG. 1 is a somewhat schematic illustration of a method of fabricatingnano-catalysts.

FIG. 2 is a somewhat schematic illustration of a method of fabricatingnano-catalysts.

FIG. 3 is a somewhat schematic illustration of a method of fabricationnano-catalysts.

FIG. 4 is a somewhat schematic illustration of a method of fabricatingnano-catalysts.

FIG. 5 is a photomicrograph of nano-catalysts.

FIGS. 6A and 6B are photomicrographs of nano-catalysts.

DETAILED DESCRIPTION

In the following detailed description of the preferred embodiments,reference is made to the accompanying drawings, which form a parthereof, and within which are shown by way of illustration the practiceof specific embodiments of methods of fabricating nano-catalysts. It isto be understood that other embodiments may be utilized, and thatstructural changes may be made and processes may vary in otherembodiments.

Disclosed herein are various processes for fabricating nano-catalyststhat have utility for forming nanostructures and manufacturingnanomaterials. In some embodiments the nano-catalysts includenanoparticles that are disposed adjacent the surface of powderparticles. The nanoparticles are typically metal. The powder particlesare typically metal or ceramic particles. Nano-catalysts that havenanoparticles disposed adjacent the surface of powder particles are anexample of powder-based nano-catalysts.

Powder-based nano-catalysts may be used in various processes to producenanostructures and nanomaterials. For example, powder-basednano-catalysts may be used to grow carbon nanotubes that may beharvested and used as nanomaterials. The powder-based nano-catalysts mayalso be incorporated as a constituent of components and coatings thatthen have catalytic properties for enhancing the formation ofnanostructures within the component or the coating. That is, instead offirst fabricating and collecting nanostructures as nanomaterials andthen mixing those nanomaterials with other constituents to formnanostructure-bearing composite materials, powder-based nano-catalystsmay be mixed with other constituents and nanostructures may then begrown in-situ to form nanostructure-bearing composite materials. Theterm “in-situ” refers a formation of nanostructures (e.g., carbonnanotubes) on individual powder particles that may subsequently be usedto fabricate composite materials that incorporate the anchorednanostructure material, without transferring the nanostructures toanother material or powder for such use. The nanostructure-bearingcomposite material may be formed as a layer that is disposed adjacentthe surface of a component or the nanostructure-bearing compositematerial may be formed as a portion or all of the bulk material of thecomponent.

Chemical processes may be used to form nanoparticles adjacent thesurface of powder materials of interest. That is, the powder materialsof interest may be chemically treated in a solution to deposit nano-sizecatalyst particles adjacent the surface of the powders by precipitationor reactive precipitation processes. Such techniques may be applied tovirtually any ceramic or metal powders or powders formed fromcombinations of metals and ceramics. For example, all Sc containingmetals, alloys, and intermetallics; all Ni containing metals, alloys,and intermetallics; all Fe containing metals, alloys, andintermetallics; all Cr containing metals, alloys, and intermetallics;all Co containing metals, alloys, and intermetallics; all Ti containingmetals, alloys, and intermetallics; all V containing metals, alloys, andintermetallics; all Mn containing metals, alloys, and intermetallics;all Cu containing metals, alloys, and intermetallics; and all Zncontaining metals, alloys, and intermetallics may be used. Y, Zr, Nb,Ru, Rh, Pd, Hf, Ta, W, Re, Ir, Pt, and Au containing metals, alloys, andintermetallics may also be used, as well as, Ce, Th, and U containingmetals, alloys, and intermetallics.

The following provides detailed descriptions of various embodiments,including nanoparticle generation and the production of nano-catalystsby deposition of the nanoparticles on the surface of selected metal,metal alloy, or ceramic powders or powders that included mixtures ofthose materials. The powder-based nano-catalysts having nanoparticlesadjacent the surfaces of the powder particles' surfaces are referred toas metal-powder-based nano-catalysts or as ceramic-powder-basednano-catalysts depending on whether the powder is a metal or a ceramic.Powder-based nano-catalysts may also be formed from silicon or othermetalloid powders; such nano-catalysts are categorized asmetal-based-powder nano-catalysts.

The surfaces of a substrate material having the shape of a geometricsolid may also be used to support nano-size catalyst particles. Suchstructures are referred to herein as “solid-based nano-catalysts.”Solid-based nano-catalysts may utilize a silicon wafer or other ceramicmaterial as a substrate. Powder-based nano-catalysts and solid-basednano-catalysts are collectively referred to herein as “nano-catalysts.”

To facilitate the formation of nano-catalysts on the surfaces of powdersor solid substrates, a “complexing agent” may be added to the surface ofa powder or a substrate. As used herein the term “complexing agent”refers to a coupling agent, a chelating agent, or a similar chemicalstructure that facilitates the binding of metal ions to the powder orsubstrate by such mechanisms as a chemical ionic bond or a chemicalcovalent bond or a chemical coordinate covalent bond or a chemicalattraction resulting from electro-negative/positive effects. With acoupling agent, an atom (e.g., a metal ion) of the nano-catalyst isbound to a single atom (e.g., an oxygen ion) of the complexing agent,whereas with a chelating agent, an atom (e.g., a metal ion) of thenano-catalyst is bound to two or more atoms (e.g., two oxygen ions, oran oxygen ion and a nitrogen ion, or multiples of such ions) of thecomplexing agent. A carboxyl functional group (—COO⁻) is an example of acoupling agent, while ethylene diamine tetraacetic acid (EDTA) is anexample of a chelating agent.

FIG. 1 illustrates an embodiment of a process 10 for formingmetal-powder-based nano-catalysts. In a typical formulation, 100 g ofmetal powder 12 is mixed in a first solution 14. Before mixing with thefirst solution 14 the metal powder 12 may be washed with deionized water(1 liter of water is typically sufficient) to clean off residual dustand debris, although typically this is not necessary. The metal powder12 may also be washed with an acid, such as hydrochloric acid, toactivate its surface. The metal powder 12 may, for example, be NiAlpowder having particle sizes that range from about 10 nanometers toabout 100 microns in diameter. NiAl powders and other powders rangingfrom about 0.5 microns to about 60 microns in diameter are typical. Suchpowders are referred to herein as powder particles. The first solution14 typically includes (a) a mixture 16 of (1) ethanol (ranging fromabout 0 wt. % to about 50 wt. %) and (2) water (ranging from about 50wt. % to about 100 wt. %) and (b) a chelating agent 18 (ranging fromabout 0.05 wt. % to about 0.5 wt. %). The chelating agent 18 may beethylene diamine tetraacetic acid (EDTA) or a similar chemical.Generally the metal powder 12 is mixed with the first solution 14 forapproximately 30 minutes using an ultrasonic bath. The first solution 14and the metal powder 12 are then allowed to stand, typically for atleast approximately an hour up to about 6 hours (but overnight or up to12 hours is not deleterious). This mixing and soaking produces achelated metal powder 20.

The process 10 includes a step 22 that involves (a) separating thechelated metal powder 20 from the residual first solution 14, typicallyby pouring the mixture of the first solution 14 and the chelated metalpowder 20 through a filter and (b) washing the chelated metal powder 20with deionized water to remove excess chelating agent 18 that may haveaccumulated with the chelated metal powder 20. The chelated metal powder20 is then added to a second solution 24 that includes metal ions 26.The second solution 24 may be 250 ml of a 0.001M to 1M (preferably 0.1M)solution of FeCl₃, which of course contains Fe³⁺ ions. In otherembodiments solutions containing other metal ions such as Co²⁻, Co³⁺, orNi²⁺ may be used. The chelated metal powder 20 and the second solution24 are stirred for about thirty minutes to about six hours or longer andthen filtered to remove “loaded” metal powder 28 from the supernatant(residual) second solution 24. As used herein the term “loaded” refersto a configuration where ions are bound to (as in a chemical ionic bondor a chemical covalent bond or a chemical attraction resulting fromelectro-negative/positive effects) a surface of an element eitherdirectly or through an intermediate material. In this case the metalions 26 are bound to the chelated metal powder 20 by the chelating agent18. The loaded metal powder 28 may then be washed with deionized waterto remove excess Fe³⁺ ions. The wash water containing Fe³⁺ ions may beanalyzed by UV-visible spectroscopy to determine the concentration ofFe³⁺ in the wash water. The loaded metal powder 28 may then be driedunder a vacuum (step 30), or it may be air dried.

In some instances it may be desirable to determine the quantity of Fe³⁺ions that are loaded on the loaded metal powder 28. This may bedetermined by using UV-visible spectroscopy to determine theconcentration of Fe³⁺ ions that were retained in the residual secondsolution 24 after the loaded metal powder 28 was filtered from theresidual second solution 24 and the concentration of Fe³⁺ ions that werewashed from the loaded metal powder 28, and then using the volume ofeach solution to calculate the moles of Fe³⁺ that were removed by thoseprocesses, and then subtracting that removed quantity from the totalstarting quantity of moles of Fe³⁺ in the first solution 14 to determinethe number of moles of Fe³⁺ ions loaded on the loaded metal powder 28.Typically the concentration of Fe³⁺ ions (i.e., the metal ions 26)loaded on to the surface of loaded metal powder 28 (where the loadedmetal powder 28 is NiAl) is about 3×10⁻⁷ grams of Fe³⁺ per gram ofloaded metal powder 28 when the solution is approximately 0.001M FeCl₃.The loaded amount may be increased by using higher concentrations ofFeCl₃ solutions.

The final step 32 for producing a metal-powder-based nano-catalyst 34 iscontacting the dried loaded metal powder 28 with a reducing environment.In a preferred method of reducing the metal ions, the loaded metalpowder 28 may be placed under a hydrogen atmosphere containing about 4wt. % hydrogen and about 96 wt. % argon at a temperature above about400° C. (generally 500-850° C.) for at least approximately 5 minutes, toreduce the metal ions 26 and form the metal-powder-based nano-catalyst34 as metal nanoparticles 36 on the metal powder 12. Extending the timeof exposure to the reducing environment to about 30 minutes increasesthe percentage of the metal ions 26 that are reduced, and an exposuretime of approximately one hour may increase the percentage. Exposuretimes beyond about two hours have diminishing returns with approximatelytwenty four hours of exposure being the limit for any statisticallysignificant increase.

In some embodiments a ceramic-powder-based nano-catalyst may be formedusing silica (silicon dioxide) powder by producing mono-dispersed silicananoparticles that are synthesized using wet colloidal chemical methods.A chelating process or a coupling agent process may be used to attachfunctional groups to the silica particle surfaces followed by loadingmetal ions onto the functionalized silica particles. Nano-catalysts mayalso be produced from ceramic powders by washing them with saltsolutions as described herein for producing nanocatalysts from metalpowders. The ceramic-powder-based nano-catalysts may then be produced bychemical reduction of the metal ions in solution or by hydrogenreduction in the solid phase at high temperature.

FIG. 2 illustrates an embodiment of a method for fabricating aceramic-powder-based nano-catalyst. The process 50 begins with forming amicroemulsion medium 52 that typically comprises water droplets 54, oil56, and a surfactant 58. The oil 56 is typically hexanol or cyclohexaneor a mixture ranging from about 0 wt. % to about 20 wt. % hexanol andfrom about 80 wt. % to about 100 wt. % cyclohexane. The water droplets54 typically comprise from about 5 wt. % to about 15 wt. % of the totalmicroemulsion medium 52, the oil 56 typically comprises from about 50wt. % to about 90 wt. % of the total microemulsion medium 52, and thesurfactant 58 typically comprises from about 5 wt. % to about 15 wt. %of the total microemulsion medium 52. A polyethylene glycolp-tert-octylphenyl ether, such as commercially available TRITON-101® maybe used as the surfactant. Another suitable surfactant istert-octylphenoxy poly(ethyhleneoxy)ethanol sold commercially under thetrade name IGEPAL (® Canada only). In the process depicted in FIG. 2,water-in-oil microemulsions such as this serve as nanoreactors toproduce components of the ceramic-powder-based nano-catalysts.

The process 50 continues with mixing an organic silane with themicroemulsion in the presence of ammonia to form silicon dioxidenanoparticles. Typically from about 20 gr. to about 100 gr. oftetraethoxysilane (TEOS) —Si(OC₂H₅)₄ and from about 2 gr. to about 5 gr.of ammonia (NH₃) are mixed to form approximately 200 to about 1000 gr.of microemulsion medium 52 to initiate a TEOS hydrolysis process 60.That is, silicon dioxide nanospheres are grown in the water droplets 54by hydrolysis of tetraethoxysilane (TEOS) in the presence of NH₃catalysts. The reaction produces amorphous silicon dioxide nanoparticles62 that are approximately spherical and that typically range from about50 to about 500 nm in diameter, however diameters ranging from about 10nm to about 10 μm are possible.

The reactions are a follows:NH₃Si(OC₂H₅)₄+4H₂O→Si(OH)₄+4C₂H₅OHnSi(OH)₄ →nSiO₂⇓+2nH₂O

The silicon dioxide nanoparticles 62 in a reaction solution 64 are thensurface modified by hydrolysis of the organosilane (a silicon alkoxide)to form functional groups —COO⁻. A coupling agent such as a sodium saltof N-(trimethoxysilylpropyl)ethylenediamne triacetate may be added tothe reaction solution 64 in an amount ranging from about 0.2 wt. % toabout 1 wt % based on the total weight of the reaction solution 64 toinitiate a process 66 that modifies the surface of the silicon dioxidenanoparticles 62 to form functionalized silicon dioxide nanoparticles68. Typically the process involves modifying the silicon dioxidenanoparticles 62 to add functional groups, such as carboxyl functionalgroups (—COO⁻) (a coupling agent) that have enhanced affinity for metalions. After their formation the functionalized silicon dioxidenanoparticles 68 may then be removed from the reaction solution 64 by,for example, a process of destabilization (e.g., centrifugation) and thecollected particles may be washed in an alcohol and water mixture. Forsimplicity of illustration the various forms of silicon dioxidenanoparticles (68, 70, 72, and 74) shown in the lower portion of FIG. 2are portrayed as hemispheres, although in reality they are substantiallyspherical in form as shown in the upper portion of FIG. 2.

Metal ions, such as Fe³⁺, Co²⁺, and Ni²⁺, may be loaded onto the surfaceof the functionalized silicon dioxide nanoparticles wherein the metalions are substantially homogeneously attracted to, attached to, oradsorbed to the surface functional groups. For example, in a step 76 thefunctionalized silicon dioxide nanoparticles 68 may be mixed in asolution 78 comprising metal ions 80 to produce loaded silicon dioxidenanoparticles 70 wherein the metal ions are bound to (as in a chemicalionic bond or a chemical covalent bond or a chemical attractionresulting from electro-negative/positive effects) the functionalizedsilicon dioxide nanoparticles.

In this embodiment the method of fabricating a ceramic-powder-basednano-catalyst then proceeds with a step 82 for separating the loadedsilicon dioxide nanoparticles 70 from substantially all of the residualsolution 78 to produce dry loaded silicon dioxide nanoparticles 72. Forexample, the loaded silicon dioxide nanoparticles 70 may be separatedfrom substantially all of the residual solution 78 by centrifuging themixture and drying the loaded silicon dioxide nanoparticles 70 in avacuum, or air drying under a hood.

The final step 84 for producing the ceramic-powder-based nano-catalystis to expose the dried loaded silicon dioxide nanoparticles 72 to areducing environment such as by placing the dried loaded silicon dioxidenanoparticles 72 under a hydrogen atmosphere (such as an atmospherecontaining about 4 wt. % hydrogen and about 96 wt. % argon) at atemperature ranging from about 400° C. to about 1200° C. (typically fromabout 500° C. to about 850° C.) for approximately 5 minutes, to reducethe metal ions to metal and form the ceramic-powder-based nano-catalyst74 as metal nanoparticles 86 on the silicon dioxide nanoparticles 62.Extending the exposure time to a range from about 30 minutes to about 2hours may be beneficial.

FIG. 3 presents a further alternate embodiment for formingmetal-powder-based nano-catalysts. The process starts with a metalpowder 100. In some embodiments the metal powder 100 may be pre-treatedwith an acid (such as hydrochloric acid) to activate its surface. Thenas depicted in FIG. 3 the metal powder 100 may be washed with ametal-ion-containing solution 102 (e.g., a metal chloride salt solution)that typically comprises ions of iron (e.g., Fe³⁺), cobalt (e.g., Co²⁺)or nickel (e.g., Ni²⁺), or combinations of two or more such ions. Metalnitrate salts (e.g., ferric nitrate) may also be used. Some beneficialsynergism has been observed in solutions containing two or more suchions, particularly where the metal powder 100 is NiAl. Typically, themetal-ion containing solution 102 is formed from a metal salt and anacid that includes the anion of the metal salt. That is, when the metalsalt is a chloride salt, the acid is hydrochloric acid; when the metalsalt is a nitrate, the acid is nitric acid; when the metal salt is asulfate, the acid is sulfuric acid, and so forth. In some embodimentsAlCl₃ may be added to provide an excess of Cl⁻ ions, which are usefulfor breaking up any Al₂O₃ that may be present. Al³⁺ ions are preferablyincluded in the wash solutions to create catalysts, and AlCl₃ may beused to break up oxide coatings on aluminum, and/or to act as a Lewisacid, or/and to generate HCl acid. AlCl₃ hydrolyzes in water to form HClacid which is an etchant for many metals helping to form catalyticfeatures. It is a favorable species in aqueous metal salt solutions.AlCl₃ in water (aqueous solutions) also provides [Cl]⁻ ions or/and[AlCl₄]⁻ ions which are reactive in the depositions of the metalcatalytic spots or dots on the larger, micron-sized powder and substratesurfaces.

Also, whereas a fresh aqueous solution of FeCl₃ is naturally acidic,over time, the pH may increase as colloidal iron hydroxide (ferroushydroxide) is formed. These colloids may precipitate and cause problems.To reduce the formation of such colloids it is advantageous to adjustthe pH of a FeCl₃ solution to a pH less than approximately three. Theaddition of dilute hydrochloric acid is the preferred method of reducingthe pH. Using 0.1 M HCl or another weak acid solution (instead of water)as the washing medium stabilizes the Fe³⁺ ions and prevents theirconversion to Fe²⁺. When nitrate salts are used, dilute nitric acid ispreferable as the washing medium.

The foregoing washing process produces a loaded metal powder 104. Thatis, the loaded metal powder 104 is a metal powder having metal ions 106attached thereto. The loaded metal powder 104 is then separated from thesupernatant metal chloride ion solution and dried either by air dryingor a vacuum. The metal ions 106 on the loaded metal powder 104 may bereduced while at a temperature of about 600° C., typically using ahydrogen gas atmosphere 108 that is typically 4% H₂ and 96% Ar,typically heated to about 600° C. The reduction process typically takesabout 5 minutes but longer process times ranging from about 30 minutesto about 2 hours may be beneficial. The result is metal-powder-basedcatalyst 110 that comprises a metal powder 112 with surface metalnanoparticle catalysts 114.

As an example of the embodiment of FIG. 3 a metal powder, such as 10 gr.of NiAl powder, may be mixed with a metal salt solution, such as 10 mLof 0.001M-1M (typically 0.1M) FeCl₃, and optionally a chelating agentsuch as EDTA. Typically the mixing includes several (typically two)hours of ultrasonic agitation or ball milling for 1 to 10 minutes. Thisprocess attaches metal ions (in this case, iron ions) to the metal (inthis case NiAl) powder to create a metal-powder-based nano-catalyst. Thesolution may then be allowed to stand for several minutes up to severaldays (typically a few hours) to allow the metal-powder-basednano-catalysts to settle. The metal-powder-based nano-catalysts may thenbe separated from the solution (such as by filtering and drying in avacuum) to form loaded metal powder. The loaded metal powder may bedried in a drying oven, typically at approximately 70° C.-80° C., ordried in air or in a vacuum. The metal ions that are attached to themetal powder may be contacted with an inert gas such as argon gascontaining about 4 wt. % hydrogen to reduce the metal ions to metalnanoparticles, wherein the metal-powder-based nano-catalysts are formed.

A further method of fabricating a metal-powder-based nano-catalystincludes a step of washing a metal powder (such as NiAl) with a solutioncomprising (i) metal ions from a metal salt having an anion and (ii) anacid comprising the anion of the metal salt, to form loaded metal powderthat has metal ions. For example, the metal salt may be FeCl₃ and theacid may be (preferably dilute, such as 0.1 M) HCl that are mixed toform a 0.01-1 M (preferably 0.1M) solution of FeCl₃ to form a loadedmetal powder having metal ions (e.g., Fe ions) disposed adjacent thesurface of the powder. Then the loaded metal powder and substantiallyall of the solution comprising metal ions are separated from each otherby filtering and drying. Finally the metal ions are reduced (such as inby hydrogen) to form the metal-powder-based nano-catalyst. In someembodiments the solution having the metal ions includes a metal saltselected from the group consisting of an iron salt, a nickel salt, acobalt salt, and combinations of two or more of those metal salts. Insome embodiments the solution having the metal ions includes two or moremetal salts selected from the group consisting of an iron salt, a nickelsalt, and a cobalt salt and combinations of two or more of theforegoing. Some embodiments of this method begin with the optional stepof activating the metal powder. Processes similar to those described forforming powder-based nano-catalysts may be used for fabrication of asolid-based nano-catalyst. Solid-based nano-catalysts have metalnano-particles disposed adjacent the surface of a substrate materialhaving the shape of a geometric solid. The substrate may, for example,be a fully-dense or a porous wafer, plate, rod, honeycomb, a foam suchas a carbon or metal foam or other geometric three-dimensional body, ora similar structure. Small granular materials may be used as substratesfor solid-based nano-catalysts. The distinction between (a)“powder-based” nano-catalysts and (b) “solid-based” nano-catalysts thatuse granular substrates is based on the diameter of the substrate.Generally, if the diameter of a substrate particle is less thanapproximately 100 micrometers the resultant nano-catalyst ischaracterized as “powder-based,” whereas if the diameter of a substrateparticle is greater than approximately 100 micrometers the resultantnano-catalyst is characterized as “solid-based.” A powder or a solidsubstrate upon which nanoparticles are formed to produce nano-catalystmaterials is referred to as a support material. The support material maycomprise metal, such as NiAl, ceramic, a cermet, or silicon or othermetalloid.

In a typical process for forming a solid-based nano-catalyst a siliconwafer is washed, activated, and then modified by using a chelating agentto bind metal ions to the surface of the wafer. In alternate embodimentsthe silicon wafer may be replaced by a silicon structure having adifferent solid geometry, or may be replaced by a solid structurecomprising a different material such as a different metalloid, aceramic, or a metal. When the substrate is a metal or a metalloid thenano-catalyst is referred to as a metal-solid-based nano-catalyst, andwhen the substrate is a ceramic the nano-catalyst is referred to as aceramic-solid-based nano-catalyst. The metal ions that are bound to (asin a chemical ionic bond or a chemical covalent bond or a chemicalcoordinate covalent bond or a chemical attraction resulting fromelectro-negative/positive effects) the surface of the solid substrateare then reduced by hydrogen reduction in the solid phase at hightemperature to produce metal nanoparticles on the silicon wafer.

FIG. 4 presents a more detailed illustration of a process for forming asolid-based nano-catalyst. In the embodiment of FIG. 4 a siliconsubstrate 120 is prepared by washing the substrate in baths of one ormore of the following chemicals: ethanol, acetone, chloroform, and water(each in turn), typically using ultrasonic agitation of the bath toenhance cleaning effectiveness. Then in step 122 the surface of thesilicon substrate 120 may be exposed to dilute (from about 0.1 to about2 molar) nitric acid, typically for a time ranging from about 30 minutesup to about 6 hours. Following exposure of the silicon substrate 120 tothe nitric acid, as a further portion of step 122, any residual nitricacid on the silicon substrate may be removed by washing the siliconsubstrate, typically with water and ethanol. The step 122 develops anactive surface 124 for further surface modification. An active surfaceis characterized as a surface that may be reacted with a coupling agentto form carboxyl groups on the surface.

In step 126 the active surface 124 of the silicon substrate 120 isexposed to a coupling agent that typically comprises a mixture of asilane compound and chloroform, which provide carboxyl functionalgroups. An exposure ranging from about one hour up to about 12 hours istypically sufficient to attach surface functional groups 128 and form afunctionalized substrate 130. Any excess coupling agent may be removedby washing with deionized water or ethanol. As illustrated by step 132,the functionalized substrate 130 may then be exposed to a dilute metalsalt solution, e.g., a solution ranging from about 0.001 to about 1molar FeCl₃, to load the surface of the functionalized substrate 130with metal ions 134 (e.g., Fe³⁺ ions, or Ni⁺² ions, or Co⁻² ions, orCo⁺³ ions or combinations of two or more of the four) and form a loadedsubstrate 136. In a step 138 the metal ions 134 that are bound to (as ina chemical ionic bond or a chemical covalent bond or a chemicalcoordinate covalent bond or a chemical attraction resulting fromelectro-negative/positive effects) the functionalized substrate materialare reduced, typically by placing the metal ions 134 on the loadedsubstrate 136 under flowing H₂ at a temperature greater than about 400°C. (e.g., ranging from about 400° C. up to about 1200° C., typicallyabout 600° C.) to form the nano-catalyst 140 as metal nanoparticles 142on the silicon substrate 120.

It should be noted that the processes for production of powder-basednano-catalysts may be adapted for production of solid-basednano-catalysts by substituting solid substrate material for the powdersubstrate material. Similarly the processes for production ofsolid-based nano-catalysts may be adapted for production of powder-basednano-catalysts by substituting a powder substrate material for the solidsubstrate material.

In some embodiments where a substrate (either a powder-based or asolid-based substrate) comprising NiAl is used, an aqueous solution ofan aluminum salt and a dilute acid (such as a chloride combination:AlCl₃+0.1M HCl, or a nitrate combination: Al(NO₃)₃+0.1 M HNO₃) may beused as an etchant to etch the surface of the substrate. In someembodiments the dilute acid may be used without a salt (AlCl₃ orAl(NO₃)₃). This etching process produces Ni²⁺ ions in the etchant. Thendrying the substrate in the presence of the etchant produces nano-sizedeposits comprising Ni²⁺ ions which are reduced when heated underhydrogen to produce a nano-catalyst. In addition, this salt solutionwashing process works not just for NiAl substrates, but also for anynickel-containing substrate. Salt solution washes may also be used withcarbon materials, such as foams. Furthermore, the salt solution washingprocess works for substrates comprising scandium, or titanium, orvanadium, or chromium, or manganese, or iron, or cobalt, or copper, orzinc as well as nickel. Substrates containing such metals may be etchedwith an acid, an aqueous aluminum salt solution, or a mixture of an acidand an aqueous solution of an aluminum salt. In some processes, such asthose using iron containing substrates (such as steel), dilutehydrochloric acid or dilute sulfuric acid may perform better than otheracids. It is generally beneficial to use dilute acids. For example,concentrated nitric acid may undesirably passivate some substratescomprising scandium, or titanium, or vanadium, or chromium, ormanganese, or iron, or cobalt, or nickel, or copper, or zinc.

Further, note that any etchant that is typically used in microscopy toevolve the grain structure of a metal will work for that metal. In someembodiments, the etchant solution may include ethanol instead of waterand/or a glycerol addition for better wetting. The following areexamples of etching processes that may be used for iron- andiron-alloy-containing materials:

-   -   a. Etch an iron- or iron-alloy-containing powder or solid        substrate in 100 ml of ethanol+1-10 ml nitric acid (not to        exceed 10% nitric acid) for a few seconds up to a few minutes.    -   b. Etch an iron- or iron-alloy-containing powder or solid        substrate in 50 ml cold-saturated (in distilled water) sodium        thiosulfate solution and 1 gr. potassium metabisulfite;        immersion at room temperature for approximately 40 seconds to        120 seconds.    -   c. Etch an iron- or iron-alloy-containing powder or solid        substrate in 80 ml ethanol+10 ml nitric+10 ml hydrochloric        acid+1 gr. Picric acid for a few seconds up to a few minutes.    -   d. Etch an iron- or iron-alloy-containing powder or solid        substrate in 30 gr. K₃Fe(CN)₆+30 gr. KOH+150 ml H₂O (1 sec to        several minutes). Note, the potassium hydroxide should be mixed        into the water before adding K₃Fe(CN)₆.    -   e. Etch an iron- or iron-alloy-containing powder or solid        substrate in 20-30 ml HCl+1-3 ml selenic acid+100 ethanol at        room temperature for 1-4 minutes.    -   f. Etch an iron- or iron-alloy-containing powder or solid        substrate in 45 ml Glycerol+15 ml HNO₃+30 ml HCl for a few        seconds up to a few minutes.    -   g. Etch an iron- or iron-alloy-containing powder or solid        substrate in 10 gr. K₃Fe(CN)₆+10 gr. KOH+100 ml water for a few        seconds up to a few minutes.

When a powder-based or a solid-based substrate is washed (etched) withan acid, an aqueous aluminum salt solution, or a mixture of an acid andan aqueous solution of an aluminum salt, the metal ion (salt)precipitates out as nano-size spots or dots. Then the metal ions arereduced to the “free” or uncharged state to form metal nano-catalystswhen heated under a hydrogen gas flow. In some embodiments where suchnano-catalysts are used to produce carbon nanotubes the hydrogen gasflow is applied both (a) during the reduction of the precipitated metalions (nano-size spots or nano-size dots) to metal nano-catalysts andalso (b) during a subsequent ethanol (or other organic) gas flow overthe nano-catalysts to form carbon nanotubes. Having hydrogen presentduring the formation of carbon nanotubes prevents the catalysts frombecoming “dead” and allows the metal nanoparticles to remain active ascatalysts for extended periods of time thereby allowing the high volumeof carbon nanotubes to be grown. This process makes the catalysts veryefficient. The same technique of flowing hydrogen gas during theformation, growth and production of carbon nanotubes may be applied toprocesses using other nano-catalysts that were generated by mechanical,thermal, or chemical means to prolong the “active life” of the catalystsand thus prolong the growth/production of carbon nanotubes.

EXAMPLES

FIG. 5 depicts an example of ceramic-powder-based nano-catalysts 150.Silicon dioxide spheres 152 have iron nanoparticles 154 disposedadjacent the surface of the silicon dioxide spheres 152. The silicondioxide spheres 152 range in diameter from about 10 nm to about 10microns (typically 50 nm-500 nm) and the iron nanoparticles 154 range indiameter from approximately 1 nm up to about 10-30 nm, but some ironnanoparticles 154 may be as large as 50 nm. The nano-catalysts 150 werefabricated by preparing a microemulsion media using polyethylene glycolp-tert-octylphenyl ether, hexanol, cyclohexane, and water. Thiswater-in-oil microemulsion served as a nanoreactor to confine theresulting nanoparticle sizes. Ceramic nanospheres were grown in themicroemulsion by hydrolysis of organic tetraethoxysilane (TEOS) in thepresence of an ammonia (NH₃) catalyst. The reaction produced amorphous,spherical nanoparticles of SiO₂. The SiO₂ surfaces were then modified byhydrolysis of the organic silane with functional groups to enhance theaffinity of the SiO₂ surfaces for metal ions. The functionalized silicaparticles were then exposed to a dilute solution of FeCl₃ wherein Fe³⁺ions were substantially homogeneously adsorbed on the surface of theSiO₂ particles by attachment to the —COO⁻ functional groups. The metalions were then reduced in the presence of hydrogen at high temperatureforming the iron nanoparticles 154 adjacent the surface of the silicondioxide spheres 152.

FIGS. 6A and 6B depict scanning electron microscope images of NiAlparticles 160 having Fe nano-catalyst particles 162 disposed on thesurfaces thereof. FIG. 6A is a backscattered electron image.

In summary, embodiments disclosed herein provide various methods forfabricating nano-catalysts. The nano-catalysts may be powder-based ormay be solid-based. The substrate powders or solids may comprise metal,ceramic, or silicon or other metalloid.

The foregoing descriptions of embodiments have been presented forpurposes of illustration and exposition. They are not intended to beexhaustive or to limit the embodiments to the precise forms disclosed.Obvious modifications or variations are possible in light of the aboveteachings. The embodiments are chosen and described in an effort toprovide the best illustrations of principles and practical applications,and to thereby enable one of ordinary skill in the art to utilize thevarious embodiments as described and with various modifications as aresuited to the particular use contemplated. All such modifications andvariations are within the scope of the appended claims when interpretedin accordance with the breadth to which they are fairly, legally, andequitably entitled.

What is claimed is:
 1. A method of fabricating a nano-catalystcomprising: (a) washing a silicon metalloid substrate material with oneor more materials selected from the group consisting of ethanol,acetone, chloroform, and water to form a treated substrate material; (b)contacting the treated substrate material with nitric acid to provide anactivated substrate material having an active silicon surface; (c)contacting the activated substrate material with a complexing agent toprovide a complexed substrate material having functionalized groups onthe active silicon surface; (d) contacting the complexed substratematerial with metal ions wherein at least a portion of the metal ionsare bound to the complexed substrate material; and (e) contacting themetal ions bound to the complexed substrate material with a reducingatmosphere to form the nano-catalyst as metal nanoparticles on thesubstrate material.
 2. The method of claim 1 wherein the substratematerial comprises a silicon wafer.
 3. The method of claim 1 wherein thecomplexing agent comprises a chelating agent.
 4. The method of claim 1wherein the complexing agent comprises a coupling agent.
 5. The methodof claim 1 wherein the complexing agent comprises a mixture ofchloroform and a silane compound.
 6. The method of claim 1 wherein thefunctionalized groups on the active silicon surface comprises carboxylfunctional groups.
 7. The method of claim 1 wherein the reducingatmosphere is at a temperature of about 600° C.
 8. A method offabricating a nano-catalyst comprising: (a) contacting a siliconmetalloid substrate material with nitric acid to provide an activatedsubstrate material having an active silicon surface; (b) contacting theactivated substrate material with a complexing agent to provide acomplexed substrate material having functionalized groups on the activesilicon surface; (c) contacting the complexed substrate material withmetal ions wherein at least a portion of the metal ions are bound to thecomplexed substrate material; and (d) contacting the metal ions bound tothe complexed substrate material with a reducing atmosphere to form thenano-catalyst as metal nanoparticles on the substrate material.